Logic applied to making isothermal assumption

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SUMMARY

The discussion focuses on the thermal analysis of a cylindrical heater system involving a long circular rod and a concentric tube. The rod has a thermal conductivity of kA = 0.15 W/(m*K), while the tube has kB = 1.5 W/(m*K) and is subjected to convection with a heat transfer coefficient of 50 W/(m²*K). The required electrical power per unit length to maintain the outer surface of the tube at 15°C is calculated to be 376.98 W/m, while the temperature at the center of the rod is determined to be 42.73°C. The isothermal assumption is justified through steady-state heat conduction principles, indicating that the interior temperature remains constant when the surface temperature is uniform.

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  • Understanding of thermal conductivity and heat transfer principles.
  • Familiarity with cylindrical coordinates and heat conduction equations.
  • Knowledge of convection heat transfer and associated coefficients.
  • Ability to perform mathematical integration in the context of thermal analysis.
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  • Learn about thermal contact resistance and its effects on heat transfer in cylindrical systems.
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Homework Statement


A thin electrical heater is inserted between a long circular rod and a concentric tube with inner and outer radii of 20 and 40 mm. The rod (A) has a thermal conductivity of kA = 0.15 W/(m*K), while the tube (B) has a thermal conductivity of kB = 1.5 W/(m*K) and its outer surface is subjected to convection with a fluid of temperature T∞ = -15°C and heat transfer coefficient 50 W/(m2 *K). The thermal contact resistance between the cylinder surfaces and the heater is negligible.
(a) Determine the electrical power per unit length of the cylinders (W/m) that is required to maintain the outer surface of cylinder B at 15°C.
(b) What is the temperature at the center of cylinder A?

Homework Equations


Rconv = 1/(hA)
Rconduction = ln(r2/r1)/(2piLk)
Q=delT/R

The Attempt at a Solution


a) Q is constant throughout cylinder.
L=length of cylinder
Rconv = 1/(50*2pi*.04*L)=.07958/L
Ts=outer surface temp
Q/L = (Ts-Tinfinity)/(L*Rconv) = 376.98 W/m
b)
T1 is temperature of the inner surface
Q/L=(T1-Ts)/(Rconduction*L)
Rconduction = ln(.04/.02)/(2*pi*L*1.5)=.07355/L
T1=(Q/L)*(Rconduction*L)+Ts = 42.73C

The answer for temperature at the center is 42.73 which is also the temperature of the outer radius of the rod.

What leads one to an isothermal assumption that allows for correct calculation?
 
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The steady state heat conduction equation for the rod is:
$$\frac{1}{r}\frac{d}{dr}\left(r\frac{dT}{dr}\right)=0$$
If we integrate this once, we obtain: $$r\frac{dT}{dr}=C$$where C is a constant. Integrating again gives:
$$T=C\ln(r)+D$$where D is another constant. If the temperature is finite at r = 0, then C must be equal to zero. Therefore, T = D = const.

Another way of answering this question is this: If a conductive body is surrounded over its entire surface by a temperature To, how can its interior temperature at steady state be anything but To?
 

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